Buildings
Advanced Kiln
Adress a wide range of industrial and chemical applications.
An advanced insulated electrical kiln in which the heat is applied by induction heating of metal.
The advantage of the induction kiln is a clean, energy-efficient and well-controllable heating process compared to most other means of fuel heating.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
800 W |
|
| Research Required: |
Smelting |
|
| Material Costs: |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
 Coal (500 kg)
|
30s |
 Refined Carbon (500 kg)
|
 Wood (800 kg)
|
30s |
Refined Carbon (500 kg)
|
 Peat (1200 kg)
|
30s |
Refined Carbon (500 kg)
|
 Clay (300 kg)
 Sand (200 kg)
|
30s |
 Ceramic (500 kg)
|
Sand (270 kg)
 Solid Visco-Gel (100 kg)
 Borax (30 kg)
|
30s |
 Fiberglass (400 kg)
|
Sand (270 kg)
 Plastic (100 kg)
Borax (30 kg)
|
30s |
Fiberglass (400 kg)
|
Sand (270 kg)
 Bioplastic (100 kg)
Borax (30 kg)
|
30s |
Fiberglass (400 kg)
|
Sand (270 kg)
 Plastium (100 kg)
Borax (30 kg)
|
30s |
Fiberglass (400 kg)
|
 Bitumen (100 kg)
 Fullerene (25 kg)
 Isosap (15 kg)
 Rayon Fiber (x10)
|
30s |
 Carbon Composite (150 kg)
|
 Oil Shale (500 kg)
|
40s |
 Cement (350 kg)
 Crude Oil (25 kg)
 Low-Grade Metallic Sand (50 kg)
|
Clay (300 kg)
Sand (200 kg)
|
30s |
 Brick (500 kg)
|
An improved refinery capable of bulk smelting process, as well exclusive metal production.
An advanced method for production of Refined Metals from raw Metal Ore.
Significantly Heats and exclusively uses Super Coolant piped into it.
Duplicants will not fabricate items unless recipes are queued.
|
|
|
 |
Dimensions: |
3 wide x 5 high |
| Power Consumption: |
3 kW |
|
| Research Required: |
Superheated Forging |
|
| Material Costs: |
| Steel or Hardened Alloy | 1000 kg | | Ceramic | 600 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Super Coolant Input Pipe | Liquid Output Pipe |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
 Copper Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Copper (370 kg)
 Slag (130 kg)
|
 Cobalt Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Cobalt (370 kg)
Slag (130 kg)
|
 Wolframite (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Tungsten (370 kg)
Slag (130 kg)
|
 Silver Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Silver (370 kg)
Slag (130 kg)
|
 Aluminum Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Aluminum (370 kg)
Slag (130 kg)
|
 Gold Amalgam (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Gold (370 kg)
Slag (130 kg)
|
 Zinc Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Zinc (370 kg)
Slag (130 kg)
|
 Nickel Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Nickel (370 kg)
Slag (130 kg)
|
 Thermium (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Niobium (370 kg)
Slag (130 kg)
|
 Iron Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Iron (370 kg)
Slag (130 kg)
|
 Cinnabar Ore (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Mercury (370 kg)
Slag (130 kg)
|
 Electrum (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
Gold (250 kg)
Silver (120 kg)
Slag (130 kg)
|
 Galena (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
 Lead (150 kg)
Silver (200 kg)
Slag (150 kg)
|
 Pyrite (400 kg)
Refined Carbon (50 kg)
Sand (50 kg)
|
40s |
Iron (300 kg)
Slag (200 kg)
|
Ammonia Breaker
An advanced catalytic cracking furnace which the ammonia synthesis reaction is reversed at elevated temperatures.
Break down Ammonia into Hydrogen and Nitrogen using Iron as catalyst.
The cracking process exudes a lot of heat.
IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
840 W |
|
| Research Required: |
Liquid-Based Refinement Processes |
|
| Material Costs: |
| Raw Mineral | 200 kg | | Refined Metal | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Ammonia Input Pipe | Gas Output Pipe | | - | Nitrogen Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Ammonia (1000 g/s)
Iron (10 g/s)
|
 Hydrogen Gas (750 g/s at 98°C)
 Nitrogen (250 g/s at 98°C)
 Rust (10 g/s at 34°C)
|
Ammonia Compressor
An industrial grade rotatory compressor unit that criticaly increase the pressure of a gas by reducing its volume, while cooling it down until liquid state is reached.
Compresses Ammonia gas and cool it down to liquid Ammonia. This device is also capable of storing liquid with complete insulation.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
480 W |
|
| Research Required: |
Temperature Modulation |
|
| Material Costs: |
| Ceramic | 400 kg | | Refined Metal | 200 kg |
|
|
| Storage Capacity: |
3000 kg |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Ammonia Input Pipe | Liquid Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Ammonia (500 g/s)
|
 Liquid Ammonia (500 g/s at -61°C)
|
Ball Crusher Mill (Chemical Washing)
A large sized industrial mill that crushes raw ores using steel balls and special mixture of acids. Capable to process much more than the standard mill, as well more efficient in the extraction of valuable minerals from the raw more sludge.
Crush down Raw Minerals in to useful materials and industrial ingredients.
|
|
|
 |
Dimensions: |
7 wide x 3 high |
| Power Consumption: |
800 W |
|
| Research Required: |
Superheated Forging |
|
| Material Costs: |
| Refined Metal | 300 kg | | Steel or Hardened Alloy | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Liquid Output Pipe | | Sulfuric Acid Input Pipe | - | | Nitric Acid Input Pipe | - |
|
|
Recipes
| Ingredients: |
Time: |
Random Products: |
 Sandstone (300 kg)
 Water (100 kg)
 Sulfuric Acid (50 kg)
|
50s |
 Toxic Slurry
Low-Grade Metallic Sand
 Fertilizer
|
 Sedimentary Rock (300 kg)
Water (100 kg)
Sulfuric Acid (50 kg)
|
50s |
Toxic Slurry
Low-Grade Metallic Sand
 Base-Grade Metallic Sand
|
 Shale (300 kg)
Water (100 kg)
Sulfuric Acid (50 kg)
|
50s |
Toxic Slurry
Low-Grade Metallic Sand
Base-Grade Metallic Sand
|
 Granite (300 kg)
Water (100 kg)
Sulfuric Acid (50 kg)
|
50s |
Toxic Slurry
Base-Grade Metallic Sand
|
 Igneous Rock (300 kg)
Water (100 kg)
 Nitric Acid (50 kg)
|
50s |
Toxic Slurry
Base-Grade Metallic Sand
 Sulfur
|
 Mafic Rock (300 kg)
Water (100 kg)
Nitric Acid (50 kg)
|
50s |
Toxic Slurry
Low-Grade Metallic Sand
Base-Grade Metallic Sand
 Refined Phosphorus
|
 Abyssalite (300 kg)
Water (100 kg)
Nitric Acid (25 kg)
Sulfuric Acid (25 kg)
|
50s |
Toxic Slurry
Low-Grade Metallic Sand
Base-Grade Metallic Sand
Refined Phosphorus
 Diamond
|
 Regolith (300 kg)
Water (100 kg)
Nitric Acid (50 kg)
Sulfuric Acid (50 kg)
|
50s |
Toxic Slurry
Low-Grade Metallic Sand
Base-Grade Metallic Sand
 High-Grade Metallic Sand
|
 Meteor Ore (300 kg)
Water (100 kg)
Nitric Acid (50 kg)
Sulfuric Acid (50 kg)
|
50s |
Toxic Slurry
Base-Grade Metallic Sand
High-Grade Metallic Sand
|
Carbon Dioxide Compressor
An industrial grade rotatory compressor unit that criticaly increase the pressure of a gas by reducing its volume, while cooling it down until liquid state is reached.
Compresses Carbon Dioxide gas and cool it down toLiquid Carbon Dioxide. This device is also capable of storing liquid with complete insulation.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
480 W |
|
| Research Required: |
Temperature Modulation |
|
| Material Costs: |
| Ceramic | 400 kg | | Refined Metal | 200 kg |
|
|
| Storage Capacity: |
3000 kg |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Carbon Dioxide Input Pipe | Liquid Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Carbon Dioxide (500 g/s)
|
 Liquid Carbon Dioxide (500 g/s at -56°C)
|
Carbon fueled Steam Boiler
An industrial grade boiler that generates thermal energy by burning solid fossil fuels.
Boils Water to Steam at 200 °C.
This particular boiler uses Combustustable Solids as fuel.
|
|
|
 |
Dimensions: |
3 wide x 4 high |
| Power Consumption: |
- |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 1200 kg | | Ceramic | 1000 kg |
|
|
| Storage Capacity: |
10 t |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Steam Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Combustible Solid (1500 g/s)
Water (4000 g/s)
|
 Steam (4000 g/s at 200°C)
Carbon Dioxide (200 g/s at 110°C)
|
Carbon Recycling Unit
An autonomous chemical device capable of executing both Bosch and Sabatier Reactions based on the input conditions.
Sabatier Reaction:
Liquid Carbon Dioxide, Hydrogen and Iron as catalyst. The Sabatier Reaction produce Water, Natural Gas and Rust as waste product.
Bosch Reaction:
Carbon Dioxide, Hydrogen and Iron as catalyst. The Bosch Reaction produce Steam, Graphite and Rust as waste product.
|
|
|
 |
Dimensions: |
7 wide x 4 high |
| Power Consumption: |
1000 W |
|
| Research Required: |
Portable Gases |
|
| Material Costs: |
| Ceramic | 800 kg | | Steel or Hardened Alloy | 400 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Hydrogen Gas Input Pipe | Liquid Output Pipe | | Liquid Carbon Dioxide Input Pipe | Steam Output Pipe | | Carbon Dioxide Input Pipe | Natural Gas Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Liquid Carbon Dioxide (200 g/s)
Hydrogen Gas (600 g/s)
Iron (25 g/s)
|
Water (500 g/s at 64°C)
 Natural Gas (300 g/s at 94°C)
Rust (25 g/s at 46°C)
|
| Inputs: |
Outputs: |
Carbon Dioxide (400 g/s)
Hydrogen Gas (400 g/s)
Iron (25 g/s)
|
Steam (400 g/s at 109°C)
 Graphite (300 g/s at 46°C)
Rust (25 g/s at 46°C)
|
Chemical Mixing Unit
This chemical fabricator has several functions in petrochemical industry.
An industrial aparatus capable to address several chemical reactions. Its large array of pipes allows safe handling of dangerous liquids and gases.
|
|
|
 |
Dimensions: |
6 wide x 4 high |
| Power Consumption: |
800 W |
|
| Research Required: |
Emulsification |
|
| Material Costs: |
| Steel or Hardened Alloy | 400 kg | | Refined Metal | 600 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Nitrogen Input Pipe | Liquid Output Pipe | | Ammonia Input Pipe | Isopropane Output Pipe | | Propane Gas Input Pipe | - | | Water Input Pipe | - | | Petroleum Input Pipe | - |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
Sulfur (20 kg)
Water (30 kg)
|
20s |
Sulfuric Acid (50 kg)
|
Nitrogen (20 kg)
Water (30 kg)
|
20s |
Nitric Acid (50 kg)
|
 Petroleum (30 kg)
Nitrogen (19 kg)
Fullerene (1000 g)
|
40s |
 Super Coolant (50 kg)
|
 Propane Gas (50 kg)
Petroleum (49 kg)
Fullerene (1000 g)
|
40s |
 Isopropane (100 kg)
|
Ammonia (5 kg)
 Dirt (35 kg)
Refined Phosphorus (5 kg)
Sulfur (5 kg)
|
20s |
Fertilizer (50 kg)
|
CO2 Filter
A fancy pump capable to detects Carbon Dioxide and pump it.
Automatically detects trace of Carbon Dioxide and extract it out of the surroudings.
|
|
|
 |
Dimensions: |
1 wide x 1 high |
| Power Consumption: |
10 W |
|
| Research Required: |
Agriculture |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| - | Gas Output Pipe |
|
|
Crude Oil Refinery
An industrial process plant responsible for refining raw oil extracted from wells.
This refinement plant is capable of the following production from Crude Oil:
- 50% Petroleum
- 25% Naphtha
- 10% Natural Gas
- 10% Sour Water waste.
- 5% Bitumen waste.
The process requires Steam for the operation.
IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
4 wide x 5 high |
| Power Consumption: |
640 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 300 kg | | Steel or Hardened Alloy | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Crude Oil Input Pipe | Petroleum Output Pipe | | Steam Input Pipe | Sour Water Output Pipe | | - | Liquid Naphtha Output Pipe | | - | Natural Gas Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Crude Oil (10 kg/s)
Steam (500 g/s)
|
Petroleum (5 kg/s at 98°C)
 Liquid Naphtha (2500 g/s)
Natural Gas (1000 g/s at 115°C)
Bitumen (500 g/s)
 Sour Water (1000 g/s)
|
Electric Steam Boiler
A small sized eletric boiler.
Boils Water to Steam at 106 °C. This particular boiler uses electricity.
|
|
|
 |
Dimensions: |
2 wide x 3 high |
| Power Consumption: |
850 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Ceramic | 200 kg | | Refined Metal | 100 kg |
|
|
| Storage Capacity: |
100 kg |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Steam Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Water (1000 g/s)
|
Steam (1000 g/s at 106°C)
|
Endothermic Unit
A device that uses endothermical chemical reaction to cool itself and its surroundings.
Creates an endothermical reaction from a mixture of Nitrate Nodules and Water.
Outputs Ammonium Water as result.
|
|
|
 |
Dimensions: |
2 wide x 2 high |
| Power Consumption: |
50 W |
|
| Research Required: |
Liquid Tuning |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Liquid Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Water (890 g/s)
 Nitrate Nodules (110 g/s)
|
 Ammonium Water (1000 g/s)
|
Ethanol Polymer Press
A custom polymerization press capable of producing polymer from Ethanol.
Special modifications allows the polymerization of Ethanol into raw Plasticwith the addition of Chlorine Gas.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
240 W |
|
| Research Required: |
Plastic Manufacturing |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Ethanol Input Pipe | Gas Output Pipe | | Chlorine Gas Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Ethanol (2500 g/s)
 Chlorine Gas (100 g/s)
|
Plastic (500 g/s at 75°C)
Steam (250 g/s at 200°C)
|
Flocculation Sieve
A dedicated industrial sieve that flocculates colloidal particles out of suspension to sediment under the form of floc. Strong filter media further improves the cleaning process of liquids.
Treat Polluted Water or Toxic Slurry using special filter and chemicals. Sieve process also completely removesGerms.
|
|
|
 |
Dimensions: |
4 wide x 3 high |
| Power Consumption: |
240 W |
|
| Research Required: |
Liquid-Based Refinement Processes |
|
| Material Costs: |
| Steel or Hardened Alloy | 200 kg | | Plastics | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Chlorine Gas Input Pipe | Liquid Output Pipe | | Polluted Water Input Pipe | - | | Toxic Slurry Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Polluted Water (5 kg/s)
Chlorine Gas (2500 mg/s)
 Crushed Rock (24 g/s)
Refined Carbon (34 g/s)
Sand (42 g/s)
|
Water (4900 g/s at -273.15°C)
Clay (110 g/s at -273.15°C)
|
| Inputs: |
Outputs: |
Toxic Slurry (5 kg/s)
Chlorine Gas (2500 mg/s)
Crushed Rock (24 g/s)
Refined Carbon (34 g/s)
Sand (42 g/s)
|
Water (2000 g/s at -273.15°C)
Slag (3100 g/s at -273.15°C)
|
Gas-fueled Steam Boiler
An industrial grade boiler that generates thermal energy by burning Combustible Gases.
Boils Water to Steam at 200 °C. This particular boiler uses Combustible Gases as fuel, but may as well work with other combustible gases.
|
|
|
 |
Dimensions: |
3 wide x 4 high |
| Power Consumption: |
- |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 1200 kg | | Ceramic | 1000 kg |
|
|
| Storage Capacity: |
10 t |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Steam Output Pipe | | Combustible Gas Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Combustible Gas (101.3 g/s)
Water (4000 g/s)
|
Steam (4000 g/s at 200°C)
Carbon Dioxide (200 g/s at 110°C)
|
Glass Foundry
A plasma arc furnace uses low-temperature plasma flow created by an electric arc heater (plasmatron).
This techlogical advanced glass foundry is capable more than melt Sand in to Molten Glass, but a wide range of other applications.
|
|
|
 |
Dimensions: |
3 wide x 3 high |
| Power Consumption: |
2.4 kW |
|
| Research Required: |
Superheated Forging |
|
| Material Costs: |
| Ceramic | 500 kg | | Refined Metal | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| - | Liquid Output Pipe |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
Sand (300 kg)
|
30s |
 Molten Glass (100 kg)
|
 Crushed Ice (500 kg)
|
10s |
Water (500 kg)
|
 Brine Ice (500 kg)
|
10s |
 Brine (500 kg)
|
 Snow (500 kg)
|
10s |
Water (500 kg)
|
 Ice (500 kg)
|
10s |
Water (500 kg)
|
 Packed Snow (500 kg)
|
10s |
Water (500 kg)
|
 Polluted Ice (500 kg)
|
10s |
Polluted Water (500 kg)
|
Jaw Crusher Mill
A jaw crusher uses compressive force for breaking of stone and other raw minerals.
Crush down Raw Minerals in to useful materials and industrial ingredients.
|
|
|
 |
Dimensions: |
3 wide x 2 high |
| Power Consumption: |
120 W |
|
| Research Required: |
Brute-Force Refinement |
|
| Material Costs: |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
 Egg Shell (5 kg)
|
20s |
 Lime (5 kg)
|
 Pokeshell Molt (1000 g)
|
20s |
Lime (10 kg)
|
 Oakshell Molt (5 kg)
|
20s |
Wood (500 kg)
|
 Fossil (100 kg)
|
40s |
Lime (5 kg)
Crushed Rock (70 kg)
Bitumen (25 kg)
|
 Salt (100 kg)
|
40s |
Borax (5 kg)
Sand (95 kg)
 Table Salt (50 g)
|
 Phosphate Nodules (100 kg)
|
40s |
Refined Phosphorus (70 kg)
Crushed Rock (30 kg)
|
Crushed Rock (100 kg)
|
30s |
Sand (100 kg)
|
 Obsidian (100 kg)
|
30s |
Sand (100 kg)
|
 Chloroschist (100 kg)
|
50s |
Crushed Rock (65 kg)
Sand (20 kg)
 Bleach Stone (500 g)
Salt (14.5 kg)
|
Shale (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Ceramic (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Igneous Rock (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Brick (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Granite (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Sedimentary Rock (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Sandstone (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Mafic Rock (100 kg)
|
40s |
Crushed Rock (100 kg)
|
Copper Ore (100 kg)
|
40s |
Copper (50 kg)
Sand (50 kg)
|
Cobalt Ore (100 kg)
|
40s |
Cobalt (50 kg)
Sand (50 kg)
|
Wolframite (100 kg)
|
40s |
Tungsten (50 kg)
Sand (50 kg)
|
Silver Ore (100 kg)
|
40s |
Silver (50 kg)
Sand (50 kg)
|
Aluminum Ore (100 kg)
|
40s |
Aluminum (50 kg)
Sand (50 kg)
|
Gold Amalgam (100 kg)
|
40s |
Gold (50 kg)
Sand (50 kg)
|
Zinc Ore (100 kg)
|
40s |
Zinc (50 kg)
Sand (50 kg)
|
Nickel Ore (100 kg)
|
40s |
Nickel (50 kg)
Sand (50 kg)
|
Thermium (100 kg)
|
40s |
Niobium (50 kg)
Sand (50 kg)
|
Iron Ore (100 kg)
|
40s |
Iron (50 kg)
Sand (50 kg)
|
Cinnabar Ore (100 kg)
|
40s |
Mercury (50 kg)
Sand (50 kg)
|
Electrum (100 kg)
|
40s |
Gold (25 kg)
Silver (15 kg)
Sand (50 kg)
|
Galena (100 kg)
|
40s |
Silver (25 kg)
Lead (15 kg)
Sand (50 kg)
|
Pyrite (100 kg)
|
40s |
Iron (30 kg)
Sand (70 kg)
|
Slag (100 kg)
Crushed Rock (20 kg)
|
40s |
Cement (80 kg)
Base-Grade Metallic Sand (12.5 kg)
High-Grade Metallic Sand (7.5 kg)
|
Multi-Stage Crude Oil Refinery
An industrial process plant responsible for refining raw oil extracted from wells.
The refinery has two stages:
First Stage: Crude Oil is first refined to:
- 50% Petroleum
- 25% Naphtha
- 10% Natural Gas
- 15% Bitumen.
Second Stage: Naphtha is furter refined:
- 45% Petroleum
- 10% Natural Gas
- 45% Bitumen.
The first stage uses Steam for the distillation process, while the second Stage uses Hydrogen to buffer the reaction.
|
|
|
 |
Dimensions: |
6 wide x 5 high |
| Power Consumption: |
640 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 500 kg | | Steel or Hardened Alloy | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Crude Oil Input Pipe | Petroleum Output Pipe | | Steam Input Pipe | Liquid Naphtha Output Pipe | | Hydrogen Gas Input Pipe | Natural Gas Output Pipe | | Liquid Naphtha Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
Crude Oil (10 kg/s)
Steam (500 g/s)
|
Petroleum (5 kg/s at 98°C)
Liquid Naphtha (2500 g/s at 94°C)
Natural Gas (500 g/s at 115°C)
Bitumen (2500 g/s at 70°C)
|
| Inputs: |
Outputs: |
Liquid Naphtha (5 kg/s)
Hydrogen Gas (250 g/s)
|
Petroleum (2000 g/s at 98°C)
Natural Gas (500 g/s at 94°C)
Bitumen (2750 g/s at 70°C)
|
Multi-Stage Raw Gas Refinery
An industrial process plant responsible for refining the impure raw natural gas extracted from wells.
The refinery has three stages:
First Stage: Raw Natural Gas is first refined to:
- 50% Natural Gas
- 40% Propane
- 10% Sour Gas
Second Stage: Propane is mixed with Hydrogen resulting in a complete conversion to Methane
Third Stage reacts the remaining Sour Gas with Nitric Acid, producing Ammonia Gas.
|
|
|
 |
Dimensions: |
8 wide x 5 high |
| Power Consumption: |
640 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 500 kg | | Steel or Hardened Alloy | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Raw Natural Gas Input Pipe | Gas Output Pipe | | Steam Input Pipe | Propane Gas Output Pipe | | Hydrogen Gas Input Pipe | Sour Gas Output Pipe | | Propane Gas Input Pipe | Ammonia Output Pipe | | Sour Gas Input Pipe | Water Output Pipe | | Nitric Acid Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Raw Natural Gas (1000 g/s)
Steam (500 g/s)
|
Natural Gas (500 g/s at 98°C)
Propane Gas (400 g/s at 94°C)
 Sour Gas (600 g/s at 115°C)
|
| Inputs: |
Outputs: |
Propane Gas (400 g/s)
Hydrogen Gas (100 g/s)
|
Natural Gas (500 g/s at 98°C)
|
| Inputs: |
Outputs: |
Sour Gas (600 g/s)
Nitric Acid (150 g/s)
|
Water (350 g/s at 89°C)
Ammonia (150 g/s at 94°C)
Sulfur (250 g/s at 60°C)
|
An industrial petrochemical plant responsible for rearranging hydrocarbon molecules of Naphtha in to Petroleum.
This second stage refinement plant is capable of furter refining Naphtha:
- 45% Petroleum
- 10% Natural Gas
- 45% Bitumen.
The process requires Hydrogen to buffer the reaction.IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
4 wide x 7 high |
| Power Consumption: |
480 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 300 kg | | Steel or Hardened Alloy | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Liquid Naphtha Input Pipe | Petroleum Output Pipe | | Hydrogen Gas Input Pipe | Natural Gas Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Liquid Naphtha (2500 g/s)
Hydrogen Gas (210 g/s)
|
Petroleum (1125 g/s at 98°C)
Natural Gas (250 g/s at 115°C)
Bitumen (1125 g/s)
|
Nitric Acid Synthesizer
A chemical synthesizer device capable of producing Nitric Acid.
Produces industrial grade Nitric Acid using provided Sulfuric Acid and Ammonia.
|
|
|
 |
Dimensions: |
1 wide x 4 high |
| Power Consumption: |
240 W |
|
| Research Required: |
Emulsification |
|
| Material Costs: |
| Ceramic | 100 kg | | Refined Metal | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Ammonia Input Pipe | Liquid Output Pipe | | Sulfuric Acid Input Pipe | Steam Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Ammonia (600 g/s)
Sulfuric Acid (500 g/s)
|
Nitric Acid (500 g/s at 72°C)
Sulfur (300 g/s at 47°C)
Steam (200 g/s at 119°C)
|
Plasma Furnace
An advanced pyrometallurgical furnace that uses an extremely hot thermal plasma generated by a carrier gas jet. The high energy consumption is compensated by the quality and the yield of the refining process.
An advanced method for the refinement of Metal Ores and other Raw Minerals.
Produces significant amounts of Heat and consumes carrier gases during manufacturing.
Main products are dispensed in molten state directly in the floor below the building while the liquid waste is released in a separated port.
|
|
|
 |
Dimensions: |
5 wide x 5 high |
| Power Consumption: |
5 kW |
|
| Research Required: |
Catalytics |
|
| Material Costs: |
| Ceramic | 2000 kg | | Tungsten | 1000 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Carrier Gas Input Pipe | Glass Output Pipe | | - | Glass Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Carrier Gas (100 g/s)
|
Carbon Dioxide (25 g/s at 75°C)
|
Recipes
| Ingredients: |
Time: |
Products: |
Sand (150 kg)
Borax (10 kg)
|
10s |
Molten Glass (100 kg)
 Molten Slag (60 kg)
|
Copper Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Copper (490 kg)
Molten Slag (50 kg)
|
Cobalt Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Cobalt (490 kg)
Molten Slag (50 kg)
|
Wolframite (500 kg)
Sand (40 kg)
|
10s |
 Molten Tungsten (490 kg)
Molten Slag (50 kg)
|
Silver Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Silver (490 kg)
Molten Slag (50 kg)
|
Aluminum Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Aluminum (490 kg)
Molten Slag (50 kg)
|
Gold Amalgam (500 kg)
Sand (40 kg)
|
10s |
 Molten Gold (490 kg)
Molten Slag (50 kg)
|
Zinc Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Zinc (490 kg)
Molten Slag (50 kg)
|
Nickel Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Nickel (490 kg)
Molten Slag (50 kg)
|
Thermium (500 kg)
Sand (40 kg)
|
10s |
 Molten Niobium (490 kg)
Molten Slag (50 kg)
|
Iron Ore (500 kg)
Sand (40 kg)
|
10s |
 Molten Iron (490 kg)
Molten Slag (50 kg)
|
Electrum (500 kg)
Sand (40 kg)
|
10s |
Molten Gold (294 kg)
Molten Silver (196 kg)
Molten Slag (50 kg)
|
Galena (500 kg)
Sand (40 kg)
|
10s |
Molten Silver (294 kg)
 Molten Lead (196 kg)
Molten Slag (50 kg)
|
Pyrite (500 kg)
Sand (40 kg)
|
10s |
Molten Iron (400 kg)
Molten Slag (140 kg)
|
Iron (425 kg)
Refined Carbon (50 kg)
Lime (25 kg)
|
10s |
 Molten Steel (500 kg)
|
Abyssalite (500 kg)
Lime (20 kg)
|
20s |
Molten Tungsten (120 kg)
 Magma (380 kg)
|
An industrial petrochemical plant responsible for oxidative steam reforming process of Propane to Hydrogen.
Reforming process of Propane in to:
- 60% Hydrogen
- 30% Polluted Water waste
- 10% Carbon Dioxide waste
The process require Steam for the operation.
IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
4 wide x 7 high |
| Power Consumption: |
320 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 300 kg | | Steel or Hardened Alloy | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Propane Gas Input Pipe | Gas Output Pipe | | Steam Input Pipe | Polluted Water Output Pipe | | - | Carbon Dioxide Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Propane Gas (525 g/s)
Steam (200 g/s)
|
Hydrogen Gas (435 g/s at 98°C)
Polluted Water (217.5 g/s)
Carbon Dioxide (72.5 g/s)
|
Pyrolysis Kiln
A basic kiln that uses pyrolysis process to convert woodlogs to usable coal.
Cook Wood to Coal.
|
|
|
 |
Dimensions: |
1 wide x 2 high |
| Power Consumption: |
- |
|
| Research Required: |
Brute-Force Refinement |
|
| Material Costs: |
|
|
Element Conversion
| Inputs: |
Outputs: |
Wood (1000 g/s)
|
Coal (330 g/s at 39°C)
Carbon Dioxide (100 g/s at 97°C)
|
Raw Gas Refinery
An industrial process plant responsible for refining the impure raw natural gas extracted from wells.
This refinement plant is capable of the following production:
- 50% Natural Gas
- 35% Propane
- 15% Sour Water waste
The process requires Steam for the operation.
IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
4 wide x 5 high |
| Power Consumption: |
420 W |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 300 kg | | Steel or Hardened Alloy | 100 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Raw Natural Gas Input Pipe | Gas Output Pipe | | Steam Input Pipe | Propane Gas Output Pipe | | - | Sour Water Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Raw Natural Gas (1000 g/s)
Steam (500 g/s)
|
Natural Gas (750 g/s at 98°C)
Propane Gas (525 g/s at 94°C)
Sour Water (225 g/s)
|
Rayon Loom
A chemical loom capable of producing celulose fibers with Viscose process.
Produces Rayon Fiber from Wood pulp through a complex chemical reaction. Requires Synthetic Gas and constantly outputs Steam while operational.
|
|
|
 |
Dimensions: |
6 wide x 4 high |
| Power Consumption: |
480 W |
|
| Research Required: |
Textile Production |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Synthesis Gas Input Pipe | - |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Synthesis Gas (800 g/s)
|
Steam (25 g/s at 100°C)
|
Recipes
| Ingredients: |
Time: |
Products: |
Wood (150 kg)
|
50s |
Rayon Fiber (x1)
|
 Plant Meat (1000 g)
|
50s |
Rayon Fiber (x1)
|
 Seakomb Leaf (20 kg)
|
50s |
Rayon Fiber (x1)
|
Salt Water Mixer
A simple device capable of producing high-quality salt water.
Produces Salt Water using provided Water and Salt.
|
|
|
 |
Dimensions: |
1 wide x 4 high |
| Power Consumption: |
90 W |
|
| Research Required: |
Distillation |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Liquid Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Water (4650 g/s)
Salt (350 g/s)
|
 Salt Water (5 kg/s at 27°C)
|
Selective Arc-Furnace
A specialized furnace that heats material by means of an electric arc. Its delicate heat control structure allows mixture of metal alloys, as well separating metals from an homogeneous mixture of scraps. Since the furnace is air-cooled, it releases a lot of heat into its surroundings.
Special works with Refined Metals and in the manufacture of metal alloys.
|
|
|
 |
Dimensions: |
4 wide x 3 high |
| Power Consumption: |
1.2 kW |
|
| Research Required: |
Smelting |
|
| Material Costs: |
|
|
Recipes
| Ingredients: |
Time: |
Random Products: |
Copper (70 kg)
Zinc (30 kg)
|
40s |
|
Copper (80 kg)
Lead (15 kg)
Refined Phosphorus (5 kg)
|
40s |
|
Iron (70 kg)
Refined Carbon (20 kg)
Lime (10 kg)
|
40s |
|
Iron (70 kg)
Refined Carbon (20 kg)
Lime (5 kg)
Borax (5 kg)
|
40s |
|
Low-Grade Metallic Sand (100 kg)
Borax (10 kg)
|
50s |
Copper
Zinc
Lead
Silver
|
Base-Grade Metallic Sand (100 kg)
Borax (10 kg)
|
50s |
Aluminum
Iron
Gold
Tungsten
|
High-Grade Metallic Sand (100 kg)
Borax (10 kg)
Graphite (10 kg)
|
50s |
Tungsten
Fullerene
Niobium
|
Thermium (100 kg)
|
50s |
|
Soil Mixer
A mixer designed for uniform blending of a wide variety of solid materials, while treating them with chemicals.
A solid material mixer designed for agricultural purpose, mainly for the production of Dirt and Fertilizer.
|
|
|
 |
Dimensions: |
4 wide x 4 high |
| Power Consumption: |
480 W |
|
| Research Required: |
Agriculture |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Polluted Water Input Pipe | - | | Water Input Pipe | - | | Ammonia Input Pipe | - |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
Nitrate Nodules (25 kg)
Phosphate Nodules (25 kg)
Sulfur (25 kg)
Polluted Water (25 kg)
|
80s |
Fertilizer (100 kg)
|
Ammonia (25 kg)
Phosphate Nodules (25 kg)
Sulfur (25 kg)
Polluted Water (25 kg)
|
80s |
Fertilizer (100 kg)
|
Refined Phosphorus (50 kg)
Crushed Rock (40 kg)
Water (10 kg)
|
60s |
Phosphate Nodules (100 kg)
|
Phosphate Nodules (50 kg)
Dirt (40 kg)
Water (10 kg)
|
60s |
 Phosphorite (100 kg)
|
Crushed Rock (40 kg)
 Polluted Dirt (20 kg)
Coal (20 kg)
Water (20 kg)
|
60s |
Dirt (100 kg)
|
Crushed Rock (40 kg)
Polluted Dirt (20 kg)
Peat (20 kg)
Water (20 kg)
|
60s |
Dirt (100 kg)
|
Crushed Rock (40 kg)
Polluted Dirt (20 kg)
Wood (20 kg)
Water (20 kg)
|
60s |
Dirt (100 kg)
|
Wood (60 kg)
Crushed Rock (30 kg)
Polluted Water (10 kg)
|
60s |
Polluted Dirt (100 kg)
|
 Compressed Biomass (40 kg)
Crushed Rock (50 kg)
Water (10 kg)
|
60s |
Dirt (100 kg)
|
Sour Water Stripper
A heavy industrial device that uses a combination of pH control and heat, direct injection of steam to drives off the ammonia and hydrogen sulfide from the water. Also fitted with a filter mechanism to ensure the quality of the stripped water.
Separate clean Water from Sour Water using hot Steam.
The stripping process also produces Sour Gas from the separation.
Sand is required to further filter the water from any other contaminants it may still have, which is then released as Polluted Dirty afterwards.
IMPORTANT: The building require all pipes ports to be connected with their respective pipes in order for it to operate.
|
|
|
 |
Dimensions: |
6 wide x 4 high |
| Power Consumption: |
360 W |
|
| Research Required: |
Liquid-Based Refinement Processes |
|
| Material Costs: |
| Raw Mineral | 400 kg | | Refined Metal | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Sour Water Input Pipe | Liquid Output Pipe | | Steam Input Pipe | Sour Gas Output Pipe | | - | Ammonia Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Sour Water (5 kg/s)
Steam (250 g/s)
Sand (100 g/s)
|
Water (4250 g/s at 48°C)
Sour Gas (750 g/s at 94°C)
Ammonia (500 g/s at 83°C)
Polluted Dirt (350 g/s)
|
Sulfuric Acid Synthesizer
A chemical synthesizer device capable of producing Sulfuric Acid.
Produces industrial grade Sulfuric Acid using provided Steam and Sulfur.
|
|
|
 |
Dimensions: |
1 wide x 4 high |
| Power Consumption: |
120 W |
|
| Research Required: |
Emulsification |
|
| Material Costs: |
| Ceramic | 100 kg | | Refined Metal | 200 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Steam Input Pipe | Liquid Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Steam (400 g/s)
Sulfur (600 g/s)
|
Sulfuric Acid (1000 g/s at 72°C)
|
Syngas Refinery
A refinery capable of catalytic partial oxidation reactions to produce Syngas.
Produce Synthetic Gas from a variety of Organic and Mineral materials.
|
|
|
 |
Dimensions: |
2 wide x 4 high |
| Power Consumption: |
60 W |
|
| Research Required: |
Distillation |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| - | Gas Output Pipe | | - | Petroleum Output Pipe |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
Wood (100 kg)
|
50s |
Synthesis Gas (25 kg)
Polluted Dirt (75 kg)
|
Bitumen (100 kg)
|
50s |
Synthesis Gas (25 kg)
Refined Carbon (75 kg)
|
Oil Shale (100 kg)
|
50s |
Synthesis Gas (50 kg)
Petroleum (30 kg)
Refined Carbon (20 kg)
|
Compressed Biomass (100 kg)
|
30s |
Synthesis Gas (25 kg)
Polluted Dirt (75 kg)
|
Thermal Desalinator
A basic desalinator that uses Vapor-compression evaporation to archive the separation of clean, usable water from the solution it is currently mixed.
Uses Steam as buffer for the Desalination process of either Salt Water or Ammonium Water, releasing fresh Water and concentrated Brine in return.
|
|
|
 |
Dimensions: |
7 wide x 3 high |
| Power Consumption: |
120 W |
|
| Research Required: |
Liquid-Based Refinement Processes |
|
| Material Costs: |
| Ceramic | 600 kg | | Refined Metal | 400 kg |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Salt Water Input Pipe | Liquid Output Pipe | | Steam Input Pipe | Water Output Pipe | | Ammonium Water Input Pipe | Ammonia Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Salt Water (5 kg/s)
Steam (500 g/s)
|
Water (4350 g/s at 54°C)
Brine (1150 g/s at 74°C)
|
| Inputs: |
Outputs: |
Ammonium Water (5 kg/s)
Steam (500 g/s)
|
Water (2500 g/s at 54°C)
Brine (2450 g/s at 74°C)
Ammonia (550 g/s at 48°C)
|
Wood-fueled Steam Boiler
An industrial grade boiler that generates thermal energy by burning wood.
Boils Water to Steam at 200 °C. This particular boiler uses Wood as fuel.
|
|
|
 |
Dimensions: |
3 wide x 4 high |
| Power Consumption: |
- |
|
| Research Required: |
Fossil Fuels |
|
| Material Costs: |
| Refined Metal | 1200 kg | | Ceramic | 1000 kg |
|
|
| Storage Capacity: |
10 t |
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Input Pipe | Steam Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
Wood (3600 g/s)
Water (4000 g/s)
|
Steam (4000 g/s at 200°C)
Carbon Dioxide (500 g/s at 110°C)
|
Refined metals are necessary to build advanced electronics and technologies.
Produces Refined Metals from raw Metal Ore.
Significantly Heats and outputs the Liquid piped into it.
Duplicants will not fabricate items unless recipes are queued.
|
|
|
 |
Dimensions: |
3 wide x 4 high |
| Power Consumption: |
800 W |
|
| Research Required: |
Smelting |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Liquid Input Pipe | Liquid Output Pipe |
|
|
Recipes
| Ingredients: |
Time: |
Products: |
Pyrite (100 kg)
Coal (20 kg)
|
40s |
Iron (60 kg)
Slag (60 kg)
|
Pyrite (100 kg)
Peat (20 kg)
|
40s |
Iron (60 kg)
Slag (60 kg)
|
Galena (100 kg)
Coal (20 kg)
|
40s |
Silver (50 kg)
Lead (30 kg)
Slag (40 kg)
|
Galena (100 kg)
Peat (20 kg)
|
40s |
Silver (50 kg)
Lead (30 kg)
Slag (40 kg)
|
Electrum (100 kg)
Coal (20 kg)
|
40s |
Gold (50 kg)
Silver (30 kg)
Slag (40 kg)
|
Electrum (100 kg)
Peat (20 kg)
|
40s |
Gold (50 kg)
Silver (30 kg)
Slag (40 kg)
|
Cinnabar Ore (100 kg)
Coal (20 kg)
|
40s |
Mercury (80 kg)
Slag (40 kg)
|
Cinnabar Ore (100 kg)
Peat (20 kg)
|
40s |
Mercury (80 kg)
Slag (40 kg)
|
Iron Ore (100 kg)
Coal (20 kg)
|
40s |
Iron (80 kg)
Slag (40 kg)
|
Iron Ore (100 kg)
Peat (20 kg)
|
40s |
Iron (80 kg)
Slag (40 kg)
|
Thermium (100 kg)
Coal (20 kg)
|
40s |
Niobium (80 kg)
Slag (40 kg)
|
Thermium (100 kg)
Peat (20 kg)
|
40s |
Niobium (80 kg)
Slag (40 kg)
|
Nickel Ore (100 kg)
Coal (20 kg)
|
40s |
Nickel (80 kg)
Slag (40 kg)
|
Nickel Ore (100 kg)
Peat (20 kg)
|
40s |
Nickel (80 kg)
Slag (40 kg)
|
Zinc Ore (100 kg)
Coal (20 kg)
|
40s |
Zinc (80 kg)
Slag (40 kg)
|
Zinc Ore (100 kg)
Peat (20 kg)
|
40s |
Zinc (80 kg)
Slag (40 kg)
|
Gold Amalgam (100 kg)
Coal (20 kg)
|
40s |
Gold (80 kg)
Slag (40 kg)
|
Gold Amalgam (100 kg)
Peat (20 kg)
|
40s |
Gold (80 kg)
Slag (40 kg)
|
Aluminum Ore (100 kg)
Coal (20 kg)
|
40s |
Aluminum (80 kg)
Slag (40 kg)
|
Aluminum Ore (100 kg)
Peat (20 kg)
|
40s |
Aluminum (80 kg)
Slag (40 kg)
|
Silver Ore (100 kg)
Coal (20 kg)
|
40s |
Silver (80 kg)
Slag (40 kg)
|
Silver Ore (100 kg)
Peat (20 kg)
|
40s |
Silver (80 kg)
Slag (40 kg)
|
Wolframite (100 kg)
Coal (20 kg)
|
40s |
Tungsten (80 kg)
Slag (40 kg)
|
Wolframite (100 kg)
Peat (20 kg)
|
40s |
Tungsten (80 kg)
Slag (40 kg)
|
Cobalt Ore (100 kg)
Coal (20 kg)
|
40s |
Cobalt (80 kg)
Slag (40 kg)
|
Cobalt Ore (100 kg)
Peat (20 kg)
|
40s |
Cobalt (80 kg)
Slag (40 kg)
|
Copper Ore (100 kg)
Coal (20 kg)
|
40s |
Copper (80 kg)
Slag (40 kg)
|
Copper Ore (100 kg)
Peat (20 kg)
|
40s |
Copper (80 kg)
Slag (40 kg)
|
Oil Well (Modified)
Water pumped into an oil reservoir cannot be recovered.
Extracts Crude Oil using clean Water.
Must be built atop an Oil Reservoir.
|
|
|
 |
Dimensions: |
4 wide x 4 high |
| Power Consumption: |
240 W |
|
| Research Required: |
Plastic Manufacturing |
|
| Material Costs: |
|
|
| Building Ports: |
| Inputs: | Outputs: |
|---|
| Water Based Input Pipe | Raw Natural Gas Output Pipe | | - | Crude Oil Output Pipe |
|
|
Element Conversion
| Inputs: |
Outputs: |
 Water Based (1000 g/s)
|
Crude Oil (3400 g/s at 90°C)
Raw Natural Gas (120 g/s at 120°C)
|